US20090017340A1 - Control method for cold fuel cell system operation - Google Patents

Control method for cold fuel cell system operation Download PDF

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Publication number
US20090017340A1
US20090017340A1 US11/774,738 US77473807A US2009017340A1 US 20090017340 A1 US20090017340 A1 US 20090017340A1 US 77473807 A US77473807 A US 77473807A US 2009017340 A1 US2009017340 A1 US 2009017340A1
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fuel cell
compressor
air
temperature
flow
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US8192881B2 (en
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Matthew C. Kirklin
Prem C. Menon
Bruce J. Clingerman
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GM Global Technology Operations LLC
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GM Global Technology Operations LLC
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Priority to US11/774,738 priority Critical patent/US8192881B2/en
Priority to DE102008031969.4A priority patent/DE102008031969B4/en
Priority to CN2008101361035A priority patent/CN101345320B/en
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04007Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
    • H01M8/04014Heat exchange using gaseous fluids; Heat exchange by combustion of reactants
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04223Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids during start-up or shut-down; Depolarisation or activation, e.g. purging; Means for short-circuiting defective fuel cells
    • H01M8/04268Heating of fuel cells during the start-up of the fuel cells
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04313Processes for controlling fuel cells or fuel cell systems characterised by the detection or assessment of variables; characterised by the detection or assessment of failure or abnormal function
    • H01M8/0432Temperature; Ambient temperature
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04694Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
    • H01M8/04746Pressure; Flow
    • H01M8/04753Pressure; Flow of fuel cell reactants
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2250/00Fuel cells for particular applications; Specific features of fuel cell system
    • H01M2250/20Fuel cells in motive systems, e.g. vehicle, ship, plane
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • H01M8/04111Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants using a compressor turbine assembly
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04313Processes for controlling fuel cells or fuel cell systems characterised by the detection or assessment of variables; characterised by the detection or assessment of failure or abnormal function
    • H01M8/0438Pressure; Ambient pressure; Flow
    • H01M8/04395Pressure; Ambient pressure; Flow of cathode reactants at the inlet or inside the fuel cell
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T90/00Enabling technologies or technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02T90/40Application of hydrogen technology to transportation, e.g. using fuel cells

Definitions

  • the field to which the present disclosure generally relates includes fuel cells, fuel cell components, fuel cell control systems, and method of using and operating the same.
  • Fuel cells have been proposed as a power source for many applications, for example, as a primary power source in vehicles and the like. To meet customer expectations in vehicle applications, the fuel cell should be capable of quick start-up. At relatively high ambient temperatures (e.g. about 20° C. or above) a fuel cell stack, which may include a plurality of individual fuel cells bundled together, can be started and reach acceptable operating conditions in a reasonable amount of time. In some applications, the preferred operating temperature may be around 80° C.
  • One embodiment includes a method of operating a fuel cell system comprising a fuel cell and a compressor that provides air to the fuel cell.
  • the method comprises sensing a temperature indicative of the temperature of a fuel cell, providing a restriction in an air flow path to the fuel cell when the sensed temperature is below a threshold, and increasing the speed of the compressor to provide a desired air flow to the fuel cell.
  • increasing the speed of the compressor increases the power drawn from the fuel cell to power the compressor and helps to increase the heat of the fuel cell.
  • the increased speed of the compressor can also result in warmer air flow from the compressor that can further increase the temperature of the system components.
  • a fuel cell system comprising at least one fuel cell, a compressor having an output communicated with the fuel cell to provide a forced air flow to the fuel cell, and at least one flow controller disposed between the compressor output and the fuel cell and through which the forced air from the compressor flows to the fuel cell.
  • the flow controller may be a valve or valves that provide(s) a variable restriction of the area for air to flow through the valve(s).
  • the system may further include an air flow sensor adapted to provide a signal indicative of the flow rate of air to the fuel cell, a temperature sensor adapted to provide a signal indicative of at least one of ambient temperature or a temperature of the fuel cell, and a control system.
  • the control system may be communicated with the air flow sensor, the temperature sensor, the compressor and the valve(s) and capable of providing a signal to the valve(s) to increase the restriction to air flow through the valve(s) when the temperature sensor provides a signal indicative of a temperature below a threshold.
  • the control system may also provide a signal to control the compressor operation to provide a determined air flow to the fuel cell even when the valve(s) reduce(s) the area for air to flow therethrough.
  • FIG. 1 illustrates a control system for a fuel cell power system 10 such as may be utilized in a vehicle application.
  • the fuel cell architecture and its controls may be of any conventional or hereinafter developed form.
  • the fuel cell power system 10 includes at least one fuel cell or fuel cell cell stack 12 .
  • a compressor 14 is provided and is driven by an electric motor 16 .
  • the compressor 14 provides a forced air flow to the cathode side of the fuel cell stack 12 , and this forced air flow may be humidified in a humidifier 32 , and its pressure controlled by a pressure regulator or by feedback control of its motor using an appropriate pressure sensor 46 .
  • the forced air flow may be provided to the fuel cell stack 12 through an air cooler 18 designed to reduce the temperature of undesirably heated air so that the air flow to the fuel cell 12 is within a desired temperature range for operation of the fuel cell.
  • One or more variable flow restrictors such as flow control valves 20 , 22 , may be disposed between the compressor output and the fuel cell stack 12 to control the flow rate of the air flow to the stack 12 .
  • control valve 22 is provided in a bypass line 21 around the humidifier 32 .
  • valves 20 , 22 there are two flow control valves 20 , 22 with one valve 22 connected in parallel to the other valve 20 and the cathode humidifier 32 . Accordingly, a portion of the output air flow from the compressor 14 passes through one valve 20 and then the cathode humidifier 32 , while a separate portion bypasses the cathode humidifier 32 and passes through the second valve 22 .
  • the divided air flows converge downstream of the cathode humidifier 32 and are delivered to the fuel cell stack in a single conduit 24 , although other arrangements may be utilized.
  • control system 25 may include one or more controllers 26 operably communicated with the compressor 14 , the fuel cell stack 12 , the air flow control valves 20 , 22 and with one or more sensors to control at least certain aspects of the fuel cell power system operation.
  • the controller 26 may include one or more discreet control units which may be communicated together, or the controller may include a single controller that controls at least the functions described hereinafter.
  • An exemplary sensor that may be used with the fuel cell power system 10 includes a temperature sensor 28 that provides to the controller 26 a signal indicative of the temperature of the air entering fuel cell stack 12 , or the temperature of the fuel cell stack 12 itself or the ambient temperature, or any combination of them.
  • Another exemplary sensor may include an air flow sensor 30 that provides a signal to the controller 26 indicative of the air flow rate delivered from the compressor 14 to the fuel cell stack 12 .
  • the temperature of the fuel cell stack 12 can become lower than its desired operating temperatures for optimum power supply operation.
  • the controller 26 partially closes at least one of the air flow valves 20 , 22 to reduce the effective flow area through one or both valves.
  • the threshold can be any suitable value below the desired operating temperature of the fuel cell stack 12 . Reducing the effective flow area of one or both valves 20 , 22 tends to increase the pressure of the air flow between the compressor and valves 20 , 22 , and reduce the flow rate.
  • the compressor 14 draws power from the fuel cell stack 12 , the stack has to supply additional power to run the compressor at its increased speed and pressure ratio. Because the fuel cell stack 12 efficiency may be low during cold temperature operation, additional waste heat is generated by the stack 12 to produce the extra power for the compressor motor 16 . Accordingly, the waste heat generated by the stack 12 contributes to an increased rate of warming of the stack 12 and subsequent more efficient operation of the fuel cell system 10 . For example, as shown in FIG. 2 , significantly higher pressure ratios can be used while staying below the surge line 40 . At a corrected mass flow rate of 70 g/s, the compressor 14 in one implementation might operate with about 3.5 kW of power and have an output air temperature of about 13° C. under normal operating conditions, as noted by plot point 42 .
  • the compressor may operate with about 11.63 kW of power and an output air temperature of about 46° C. when the air flow is restricted and the compressor pressure ratio is increased; as shown by plot point 44 .
  • the compressor 14 requires over 8 kilowatts (kW) of additional power to push the same concentration of oxygen through the restricted or partially closed air flow valves 20 , 22 and to the fuel cell stack 12 compared to when the air flow valves 20 , 22 are in their normal position for normal operation of the fuel cell system 10 .
  • the stack 12 produces an increased amount of waste heat to produce the extra power for the compressor motor 16 .
  • the increased compressor speed and power consumption provides a higher temperature of the air discharged from the compressor 14 .
  • This warmer air passes through the air cooler 18 and helps heat the air cooler 18 and any cooling fluid therein.
  • the heated fluid may be circulated through the fuel cell stack 12 to heat the same.
  • the fuel cell stack 12 is further heated upon delivery of the increased temperature air flow thereto.
  • the system can be controlled so that over 8 kW of additional power can be required to drive the compressor motor 16 to deliver the same or similar mass of air to the fuel cell stack 12 during start-up compared to the power requirement without throttling down the valves 20 , 22 .
  • the 8 kW to drive the motor about 70% of that may go into the airflow, or about 5.6 kW.
  • the control system 25 may use a feed forward model to calculate the position of or relative restriction to air flow of the air flow valves 20 , 22 to maximize the compressor pressure ratio during the cold start or cold temperature operation.
  • the position of the valves 20 , 22 may be controlled as a function of a determined or desired pressure ratio of the compressor motor 16 .
  • a compressor pressure sensor 46 could also be used to provide feedback control of the position of the air flow valves based on the pressure at the outlet and/or across the compressor to determine the desired position of the valves.
  • the compressor motor 16 is preferably operated with a closed loop feedback control on the air flow sensor 30 so that the compressor speed is automatically increased to compensate for the partial closing of the air flow valves 20 , 22 . Because the total effective area of the two air flow valves 20 , 22 determines the pressure ratio of the compressor 14 , the compressor control loop can also be independent of RH controls.
  • throttling the valves 20 , 22 between the compressor 14 and the fuel cell stack 12 and then increasing the output of the compressor 14 so that the fuel cell stack 12 receives a desired air flow (e.g. a flow rate controlled as a function of a determined air flow rate)
  • additional energy can be drawn from the stack 12 to power the compressor 14 and can be delivered to the stack 12 in the form of an increased temperature air flow.
  • This improves the cold start performance and cold temperature operation of the fuel cell system 10 , and increases the rate at which the fuel cell power system temperature is increased to thereby reduce the time of low temperature fuel cell stack operation.

Abstract

A method of operating a fuel cell system comprising a fuel cell and a compressor that provides air to the fuel cell. The method comprises sensing a temperature indicative of the temperature of a fuel cell, providing a restriction in an air flow path to the fuel cell when the sensed temperature is below a threshold, and increasing the speed of the compressor to provide a desired air flow to the fuel cell. In at least some implementations, increasing the speed of the compressor increases the power drawn from the fuel cell to power the compressor and helps to increase the heat of the fuel cell. The increased speed of the compressor can also result in warmer air flow from the compressor that can further increase the temperature of the system components.

Description

    TECHNICAL FIELD
  • The field to which the present disclosure generally relates includes fuel cells, fuel cell components, fuel cell control systems, and method of using and operating the same.
  • BACKGROUND
  • Fuel cells have been proposed as a power source for many applications, for example, as a primary power source in vehicles and the like. To meet customer expectations in vehicle applications, the fuel cell should be capable of quick start-up. At relatively high ambient temperatures (e.g. about 20° C. or above) a fuel cell stack, which may include a plurality of individual fuel cells bundled together, can be started and reach acceptable operating conditions in a reasonable amount of time. In some applications, the preferred operating temperature may be around 80° C.
  • At relatively low temperatures, such as subfreezing temperatures of about −25° C., rapid startup of the fuel cell stack is more difficult because at these temperatures the rate at which the overall electrochemical reaction occurs is significantly reduced. This limits the amount of current that can be drawn from the stack and the resultant heat output by the stack. The reduced output of the fuel cell stack can degrade drive-away performance of the vehicle, as well as slow the rate at which the interior vehicle cabin can be heated, the rate at which windshield defrost mechanisms operate, and the like.
  • SUMMARY OF EXEMPLARY EMBODIMENTS OF THE INVENTION
  • One embodiment includes a method of operating a fuel cell system comprising a fuel cell and a compressor that provides air to the fuel cell. The method comprises sensing a temperature indicative of the temperature of a fuel cell, providing a restriction in an air flow path to the fuel cell when the sensed temperature is below a threshold, and increasing the speed of the compressor to provide a desired air flow to the fuel cell. In at least some implementations, increasing the speed of the compressor increases the power drawn from the fuel cell to power the compressor and helps to increase the heat of the fuel cell. The increased speed of the compressor can also result in warmer air flow from the compressor that can further increase the temperature of the system components.
  • Another embodiment of the invention includes a fuel cell system, comprising at least one fuel cell, a compressor having an output communicated with the fuel cell to provide a forced air flow to the fuel cell, and at least one flow controller disposed between the compressor output and the fuel cell and through which the forced air from the compressor flows to the fuel cell. The flow controller may be a valve or valves that provide(s) a variable restriction of the area for air to flow through the valve(s). The system may further include an air flow sensor adapted to provide a signal indicative of the flow rate of air to the fuel cell, a temperature sensor adapted to provide a signal indicative of at least one of ambient temperature or a temperature of the fuel cell, and a control system. The control system may be communicated with the air flow sensor, the temperature sensor, the compressor and the valve(s) and capable of providing a signal to the valve(s) to increase the restriction to air flow through the valve(s) when the temperature sensor provides a signal indicative of a temperature below a threshold. The control system may also provide a signal to control the compressor operation to provide a determined air flow to the fuel cell even when the valve(s) reduce(s) the area for air to flow therethrough.
  • Other exemplary embodiments of the present invention will become apparent from the detailed description provided hereinafter. It should be understood that the detailed description and specific examples, while disclosing exemplary embodiments of the invention, are intended for purposes of illustration only and are not intended to limit the scope of the invention.
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • Exemplary embodiments of the present invention will become more fully understood from the detailed description and accompanying drawings, wherein:
  • FIG. 1 schematically depicts a control system to improve the cold start performance of a fuel cell stack; and
  • FIG. 2 is a graph of compressor pressure ratio and air mass flow rate.
  • DETAILED DESCRIPTION OF EXEMPLARY EMBODIMENTS
  • Referring in more detail to the drawings, FIG. 1 illustrates a control system for a fuel cell power system 10 such as may be utilized in a vehicle application. The fuel cell architecture and its controls may be of any conventional or hereinafter developed form. In the embodiment shown in FIG. 1, the fuel cell power system 10 includes at least one fuel cell or fuel cell cell stack 12. A compressor 14 is provided and is driven by an electric motor 16. The compressor 14 provides a forced air flow to the cathode side of the fuel cell stack 12, and this forced air flow may be humidified in a humidifier 32, and its pressure controlled by a pressure regulator or by feedback control of its motor using an appropriate pressure sensor 46. The forced air flow may be provided to the fuel cell stack 12 through an air cooler 18 designed to reduce the temperature of undesirably heated air so that the air flow to the fuel cell 12 is within a desired temperature range for operation of the fuel cell. One or more variable flow restrictors, such as flow control valves 20, 22, may be disposed between the compressor output and the fuel cell stack 12 to control the flow rate of the air flow to the stack 12. In one embodiment, control valve 22 is provided in a bypass line 21 around the humidifier 32.
  • In the embodiment shown, there are two flow control valves 20, 22 with one valve 22 connected in parallel to the other valve 20 and the cathode humidifier 32. Accordingly, a portion of the output air flow from the compressor 14 passes through one valve 20 and then the cathode humidifier 32, while a separate portion bypasses the cathode humidifier 32 and passes through the second valve 22. In the embodiment shown, the divided air flows converge downstream of the cathode humidifier 32 and are delivered to the fuel cell stack in a single conduit 24, although other arrangements may be utilized.
  • In one implementation, the control system 25 may include one or more controllers 26 operably communicated with the compressor 14, the fuel cell stack 12, the air flow control valves 20, 22 and with one or more sensors to control at least certain aspects of the fuel cell power system operation. The controller 26 may include one or more discreet control units which may be communicated together, or the controller may include a single controller that controls at least the functions described hereinafter. An exemplary sensor that may be used with the fuel cell power system 10 includes a temperature sensor 28 that provides to the controller 26 a signal indicative of the temperature of the air entering fuel cell stack 12, or the temperature of the fuel cell stack 12 itself or the ambient temperature, or any combination of them. Another exemplary sensor may include an air flow sensor 30 that provides a signal to the controller 26 indicative of the air flow rate delivered from the compressor 14 to the fuel cell stack 12.
  • When the fuel cell power system 10 is subjected to relatively cold ambient temperatures, the temperature of the fuel cell stack 12 can become lower than its desired operating temperatures for optimum power supply operation. When the temperature sensed by the temperature sensor 28 is below a threshold, the controller 26 partially closes at least one of the air flow valves 20, 22 to reduce the effective flow area through one or both valves. For example, the threshold can be any suitable value below the desired operating temperature of the fuel cell stack 12. Reducing the effective flow area of one or both valves 20, 22 tends to increase the pressure of the air flow between the compressor and valves 20, 22, and reduce the flow rate. To avoid providing air at an increased pressure and a reduced flow rate to the fuel cell stack 12, the controller 26 also provides a signal to the compressor motor 16 to increase its rotational speed. In this manner, the compressor 14 requires more energy to provide the same amount of air to the fuel cell stack 12.
  • Because the compressor 14 draws power from the fuel cell stack 12, the stack has to supply additional power to run the compressor at its increased speed and pressure ratio. Because the fuel cell stack 12 efficiency may be low during cold temperature operation, additional waste heat is generated by the stack 12 to produce the extra power for the compressor motor 16. Accordingly, the waste heat generated by the stack 12 contributes to an increased rate of warming of the stack 12 and subsequent more efficient operation of the fuel cell system 10. For example, as shown in FIG. 2, significantly higher pressure ratios can be used while staying below the surge line 40. At a corrected mass flow rate of 70 g/s, the compressor 14 in one implementation might operate with about 3.5 kW of power and have an output air temperature of about 13° C. under normal operating conditions, as noted by plot point 42. The compressor may operate with about 11.63 kW of power and an output air temperature of about 46° C. when the air flow is restricted and the compressor pressure ratio is increased; as shown by plot point 44. Accordingly, in one exemplary implementation, the compressor 14 requires over 8 kilowatts (kW) of additional power to push the same concentration of oxygen through the restricted or partially closed air flow valves 20, 22 and to the fuel cell stack 12 compared to when the air flow valves 20, 22 are in their normal position for normal operation of the fuel cell system 10. And the stack 12 produces an increased amount of waste heat to produce the extra power for the compressor motor 16.
  • As noted above, the increased compressor speed and power consumption provides a higher temperature of the air discharged from the compressor 14. This warmer air passes through the air cooler 18 and helps heat the air cooler 18 and any cooling fluid therein. The heated fluid may be circulated through the fuel cell stack 12 to heat the same. The fuel cell stack 12 is further heated upon delivery of the increased temperature air flow thereto. In the example shown in FIG. 2, the system can be controlled so that over 8 kW of additional power can be required to drive the compressor motor 16 to deliver the same or similar mass of air to the fuel cell stack 12 during start-up compared to the power requirement without throttling down the valves 20, 22. In this example, of the 8 kW to drive the motor, about 70% of that may go into the airflow, or about 5.6 kW.
  • The control system 25 may use a feed forward model to calculate the position of or relative restriction to air flow of the air flow valves 20, 22 to maximize the compressor pressure ratio during the cold start or cold temperature operation. In some implementations, the position of the valves 20, 22 may be controlled as a function of a determined or desired pressure ratio of the compressor motor 16. A compressor pressure sensor 46 could also be used to provide feedback control of the position of the air flow valves based on the pressure at the outlet and/or across the compressor to determine the desired position of the valves. By maximizing or increasing the compressor pressure ratio, the amount of additional energy required to operate the compressor motor 16, and hence, the amount of additional energy required from the fuel cell stack 12, as well as a corresponding increase in the temperature of the air discharged from the compressor 14, can be controlled to facilitate warming up of the fuel cell power system 10. To maintain the air flow to the fuel cell stack 12 generally constant or within a desired range, the compressor motor 16 is preferably operated with a closed loop feedback control on the air flow sensor 30 so that the compressor speed is automatically increased to compensate for the partial closing of the air flow valves 20, 22. Because the total effective area of the two air flow valves 20, 22 determines the pressure ratio of the compressor 14, the compressor control loop can also be independent of RH controls.
  • Accordingly, by throttling the valves 20, 22 between the compressor 14 and the fuel cell stack 12, and then increasing the output of the compressor 14 so that the fuel cell stack 12 receives a desired air flow (e.g. a flow rate controlled as a function of a determined air flow rate), additional energy can be drawn from the stack 12 to power the compressor 14 and can be delivered to the stack 12 in the form of an increased temperature air flow. This improves the cold start performance and cold temperature operation of the fuel cell system 10, and increases the rate at which the fuel cell power system temperature is increased to thereby reduce the time of low temperature fuel cell stack operation.
  • The above description of embodiments of the invention is merely exemplary in nature and, thus, variations thereof are not to be regarded as a departure from the spirit and scope of the invention. By way of example without limitation, increasing the restriction to the compressor output air flow may be accomplished in ways other than partially closing one or more valves, such as by directing the air flow in full or in part through a different path when the restricted air flow is desired. Of course, still other arrangements may be utilized, as desired.

Claims (17)

1. A method of operating a fuel cell system comprising a fuel cell and a compressor that provides air to the fuel cell, the method comprising:
sensing a temperature indicative of the temperature of a fuel cell;
providing a restriction in an air flow path from the compressor to the fuel cell when the sensed temperature is below a threshold; and
increasing the speed of the compressor to provide a desired air flow to the fuel cell.
2. The method of claim 1 wherein the fuel cell system also includes a flow controller disposed between the compressor and the fuel cell, and providing a restriction in the air flow path is accomplished by the flow controller.
3. The method of claim 2 wherein the flow controller includes a valve that provides a variable restriction in the air flow path reducing the cross-section area through which air may flow.
4. The method of claim 3 which also includes sensing the pressure across the compressor and controlling the restriction as a function of a determined pressure ratio of the compressor.
5. The method of claim 1 which also includes sensing the flow rate of air at the fuel cell and controlling the output of the compressor as a function of a determined air flow rate.
6. A fuel cell system, comprising:
at least one fuel cell;
a compressor having an output communicated with the fuel cell to provide a forced air flow to the fuel cell;
at least one flow controller disposed between the compressor output and the fuel cell and through which the forced air from the compressor flows to the fuel cell, the flow controller providing a variable restriction of the area for air to flow therethrough;
an air flow sensor adapted to provide a signal indicative of the flow rate of air to the fuel cell;
a temperature sensor adapted to provide a signal indicative of at least one of ambient temperature or a temperature of the fuel cell; and
a control system communicated with the air flow sensor, the temperature sensor, the compressor and the flow controller, the control system providing a signal to the flow controller to increase the restriction to air flow through the flow controller when the temperature sensor provides a signal indicative of a temperature below a threshold, and the control system providing a signal to control the compressor operation to provide a determined air flow rate to the fuel cell even when the flow controller reduces the area for air to flow therethrough.
7. The system of claim 6 wherein the fuel cell is communicated with the compressor to provide power to the compressor to support operation of the compressor.
8. The system of claim 7 wherein when the flow controller provides a reduced area for air to flow therethrough, the control system causes the compressor to provide an output flow rate with a higher pressure ratio which increases the power draw of the compressor from the fuel cell.
9. The system of claim 8 wherein when the compressor provides an output flow rate with a higher pressure ratio, the temperature of the air discharged from the compressor is increased.
10. The system of claim 6 wherein said at least one flow controller includes two valves disposed in parallel to each other, and a humidifier disposed between one of said two valves and the fuel cell to control the humidification of the air that flows therethrough and to the fuel cell.
11. The system of claim 6 wherein the control system uses feed forward control to control the restriction provided by said at least one flow controller.
12. The system of claim 11 wherein the control system maximizes the compressor pressure ratio by controlling the air flow through said at least one flow controller.
13. The system of claim 6 which also includes a pressure sensor that provides a signal indicative of the output pressure of the compressor, the pressure sensor being communicated with the control system.
14. The system of claim 9 which also includes an air cooler disposed between the compressor and the fuel cell and wherein the increased air temperature output from the compressor flows through the air cooler and heat is transferred to a fluid flowing through the air cooler.
15. A method, comprising:
powering a compressor with a fuel cell to provide air flow to the fuel cell;
sensing a temperature indicative of the temperature of the fuel cell;
providing a restriction in an air flow path from the compressor to the fuel cell when the sensed temperature is below a threshold;
increasing the output of the compressor by providing additional power from the fuel cell to the compressor to provide a desired air flow rate to the fuel cell.
16. The method of claim 15 wherein the restricting includes reducing the effective flow area of a valve disposed between the compressor and the fuel cell.
17. The method of claim 15 which also includes sensing the pressure across the compressor and controlling the restriction to air flow to the fuel cell as a function of the pressure across the compressor.
US11/774,738 2007-07-09 2007-07-09 Control method for cold fuel cell system operation Active 2030-02-13 US8192881B2 (en)

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DE102008031969.4A DE102008031969B4 (en) 2007-07-09 2008-07-07 Method for operating a fuel cell system and correspondingly adapted fuel cell system
CN2008101361035A CN101345320B (en) 2007-07-09 2008-07-09 Control method for cold fuel cell system operation

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CN101345320A (en) 2009-01-14

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